EP2222845A2 - Mikroorganismen für erhöhte ethanol- und butanolproduktion sowie verfahren zur herstellung von ethanol und butanol damit - Google Patents

Mikroorganismen für erhöhte ethanol- und butanolproduktion sowie verfahren zur herstellung von ethanol und butanol damit

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Publication number
EP2222845A2
EP2222845A2 EP08865113A EP08865113A EP2222845A2 EP 2222845 A2 EP2222845 A2 EP 2222845A2 EP 08865113 A EP08865113 A EP 08865113A EP 08865113 A EP08865113 A EP 08865113A EP 2222845 A2 EP2222845 A2 EP 2222845A2
Authority
EP
European Patent Office
Prior art keywords
butanol
coa
ethanol
recombinant microorganism
enhanced ability
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP08865113A
Other languages
English (en)
French (fr)
Other versions
EP2222845A4 (de
Inventor
Sang Yup Lee
Yu-Sin Jang
Jin Young Lee
Kwang Seop Jung
Jae Hyun Kim
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Korea Advanced Institute of Science and Technology KAIST
Biofuelchem Co Ltd
GS Caltex Corp
Original Assignee
Korea Advanced Institute of Science and Technology KAIST
Biofuelchem Co Ltd
GS Caltex Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Korea Advanced Institute of Science and Technology KAIST, Biofuelchem Co Ltd, GS Caltex Corp filed Critical Korea Advanced Institute of Science and Technology KAIST
Publication of EP2222845A2 publication Critical patent/EP2222845A2/de
Publication of EP2222845A4 publication Critical patent/EP2222845A4/de
Withdrawn legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/065Ethanol, i.e. non-beverage with microorganisms other than yeasts
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N15/00Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09Recombinant DNA-technology
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004Oxidoreductases (1.)
    • C12N9/0006Oxidoreductases (1.) acting on CH-OH groups as donors (1.1)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/10Transferases (2.)
    • C12N9/13Transferases (2.) transferring sulfur containing groups (2.8)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/16Butanols
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • the present invention relates to a recombinant microorganism having an enhanced ability to produce ethanol and butanol and a method for preparing ethanol and butanol using the same, and more particularly to a recombinant microorganism having an enhanced ability to produce ethanol and butanol, into which a gene encoding CoA transferase and a gene encoding alcohol/aldehyde dehydrogenase are introduced, and a method for preparing ethanol and butanol using the same.
  • ethanol(C 2 H 5 OH) has been prepared by a method of fermenting starch or sugars, and most alcoholic beverages theses days are prepared by such a method.
  • ethanol is currently being prepared by synthetic methods comprising using ethylene (ethene) obtained from petroleum as a raw material: a sulfuric acid hydrolysis method in which ethylene is absorbed into sulfuric acid to produce the sulfuric acid ester of ethanol, then hydrolyzed to produce ethanol together with diethyl ether, and a direct hydration method in which ethylene in a gaseous phase is allowed to react with aqueous vapor by contact using a solid phosphoric acid catalyst, thereby leading to direct synthesis of ethanol.
  • said methods have disadvantages i in that petroleum is a basic raw material, and that in the case of the sulfuric acid hydrolysis method, large scale facilities are required for the concentration and circulation of a large amount of sulfuric acid.
  • butanol C 4 H 9 OH
  • ethanol chemical synthesis of butanol also uses petroleum as a raw material to produce propylene, which is used to synthesize butanol by the oxo process.
  • propylene Such a method involving high temperature and high pressure, using petroleum as a raw material, is inefficient in both cost and energy (Tsuchida et al, Ind. Eng. Chem. Res., 45:8634, 2006).
  • a plasmid (pFNK6) was prepared by introducing 3 genes: a gene ⁇ adc) encoding acetoacetic acid decarboxylase, a gene (ctfA) encoding CoA transferase A and a gene (ct ⁇ B) encoding CoA transferase B into a vector and constructing an artificial operon using an adc promoter, and the plasmid was introduced into Clostridium acetobutylicum ATCC 824, thereby improving the productivity of acetone, butanol and ethanol by 95%, 37% and 90%, respectively, compared to the wild-type (Mermelstein et al, Biotechnol.
  • Clostridium beijerinckii BAlOl which is a mutant strain obtained through random mutagenesis, was fermented using maltodextrins as a carbon source, and was reported to have produced 18.6 g/1 of butanol (Ezeji et al, Appl Microbiol. Biotechnol, 63:653,
  • the present inventors have made extensive efforts to develop microorganisms capable of producing ethanol and butanol with high yield without producing byproducts based on the pathway for ethanol and butanol synthesis (FIG. 1), and as a result, constructed a recombinant microorganism by cloning two enzymes derived from Clostridium acetobutylicum ATCC 824: (1) ctfAS> encoding CoA transferase, which converts acetic acid and butyric acid into acetyl CoA and butylyl CoA, respectively, and (2) adhEl encoding alcohol/aldehyde dehydrogenase, which converts acetyl CoA and butyryl CoA into ethanol and butanol, respectively, and introducing the cloned genes into a host microorganism incapable of producing organic solvents, and confirmed that the recombinant microorganism produces high concentrations of ethanol and butanol while producing almost no acetone as
  • Another object of the present invention is to provide a method for preparing ethanol and butanol using said recombinant microorganism.
  • the present invention provides a method for constructing a recombinant microorganism having an enhanced ability to produce ethanol and butanol, the method comprises introducing a gene encoding an enzyme that converts acetic acid and butyric acid to acetyl CoA and butylyl CoA, respectively; and/or a gene encoding an enzyme that converts acetyl CoA and butyryl CoA to ethanol and butanol, respectively, into a host microorganism which has genes encoding enzymes involved in the biosynthetic pathway for conversion of acetyl CoA to butyryl CoA.
  • the present invention also provides a recombinant microorganism having an enhanced ability to produce ethanol and butanol, which has a gene encoding an enzyme that converts acetic acid and butyric acid to acetyl CoA and butylyl CoA, respectively; and/or a gene encoding an enzyme that converts acetyl CoA and butyryl CoA to ethanol and butanol, respectively, introduced or amplified into a host microorganism having genes encoding enzymes involved in the biosynthetic pathway for conversion of acetyl CoA to butyryl CoA.
  • the present invention provides a method for preparing ethanol and/or butanol, the method comprising the steps of culturing said recombinant microorganism and recovering ethanol and/or butanol from the culture broth.
  • FIG. 1 is a schematic diagram showing the metabolic pathway in a degenerated strain of Clostridium acetobutylicum (A), which has no ability to produce ethanol and butanol, and the metabolic pathway for the synthesis of ethanol and butanol in a recombinant strain constructed by introducing ctf AB and adhEl into the degenerated strain (B).
  • FIG. 2 is a genetic map of the recombinant vector pIMPl ::adhEl .ctfAB which contains ctf AB and adhEl.
  • the present invention relates to method for constructing a recombinant microorganism having an enhanced ability to produce ethanol and butanol, the method comprises introducing or amplifying a gene encoding an enzyme that converts acetic acid and butyric acid to acetyl CoA and butylyl CoA, respectively; and/or a gene encoding an enzyme that converts acetyl CoA and butyryl CoA to ethanol and butanol, respectively, into a host microorganism which has genes encoding enzymes involved in the biosynthetic pathway for conversion of acetyl CoA to butyryl CoA.
  • the present invention also relates to a recombinant microorganism having an enhanced ability to produce ethanol and butanol, which has a gene encoding an enzyme that converts acetic acid and butyric acid to acetyl CoA and butylyl CoA, respectively; and/or a gene encoding an enzyme that converts acetyl CoA and butyryl CoA to ethanol and butanol, respectively, introduced or amplified into a host microorganism having genes encoding enzymes involved in the biosynthetic pathway for conversion of acetyl CoA to butyryl CoA.
  • the term "amplification” is used herein broadly to refer to processes: mutation, substitution or deletion, and insertion of some base(s) of a relevant gene; or introducing a gene derived from other microorganism encoding the same enzyme to increase the activity of the corresponding enzyme.
  • said biosynthetic pathway for conversion of acetyl CoA into butyryl CoA is preferably [acetyl CoA ⁇ acetoacetyl CoA ⁇ 3- hydroxybutyryl CoA ⁇ crotonyl CoA ⁇ butyryl CoA].
  • the host microorganism preferably has an acetone biosynthetic pathway blocked and thus has acetone production of less than 10% of the total organic solvent production.
  • An adc (a gene encoding acetoacetic acid decarboxylase) may be deleted in said pathway for acetone biosynthesis, but is not limited thereto.
  • said host microorganism is preferably derived from the genus Clostridium, but it is not limited thereto as long as it has a biosynthetic pathway for conversion of acetyl CoA into butyryl CoA.
  • the enzyme converting acetic acid and butyric acid into acetyl CoA and butylyl CoA, respectively, is CoA transferase; and the gene encoding the CoA transferase is ctf. AB.
  • the enzyme converting acetyl CoA and butyryl CoA into ethanol and butanol, respectively is alcohol/aldehyde dehydrogenase; and the gene encoding the alcohol/aldehyde dehydrogenase is adhEl.
  • the present invention used only said ctf AB and adhEl derived from Clostridium acetobutylicum ATCC 824 as an example, but genes derived from other microorganisms may be used without limitation as long as they are expressed in a host cell, into which they are introduced, and have the same activities.
  • the host microorganism used is a mutant M5 strain of Clostridium acetobutylicum which lacks megaplasmid (carrying 127 genes, including a gene encoding acetoacetic acid decarboxylase, a gene encoding CoA transferase and a gene encoding alcohol/aldehyde dehydrogenase).
  • the mutant M5 strain of Clostridium acetobutylicum is a microorganism whose pathway for acetone biosynthesis is blocked (FIG. 1).
  • Clostridium acetobutylicum M5 was used as an example of the host microorganisms of the genus Clostridium whose pathway for acetone biosynthesis is blocked, but Clostridium acetobutylicum INYG, 4NYG, 5NYG and DGl (Stim- Herndon, K.P. et al, Biotechnol. /Food Microbiol., 2: 11, 1996), C. acetobutylicum ATCC 824 Type IV, M3, M5, 2-BB R, 2-BB D, Rif B 12, Rif DlO, Rif F7, and C. butyricum ATCC 860 (Clark, S. W. et al, Appl. Environ.
  • Microbiol, 55:970, 1989 may also be used.
  • the recombinant microorganism M5 pIMPl ::adhEl .ctfAB
  • pIMPl ::adhEl .ctfAB a recombinant vector carrying said ctf AB and adhEl
  • the present invention relates to a method for preparing ethanol and/or butanol, the method comprising the steps of culturing said recombinant microorganism and recovering ethanol and/or butanol from the culture broth.
  • the processes of culturing recombinant microorganisms and recovering ethanol and butanol may be performed using the conventional o culture method and the conventional method for isolation and purification of ethanol/butanol known in the fermentation art.
  • the recovery of butanol and ethanol is usually carried out after completing the culture, it may be carried out during culture in order to improve productivity, using proper methods such as gas-stripping method (Thaddeus et al., Bioprocess Biosyst. Eng., 27:207, 2005). That is, continuous culture while recovering ethanol and butanol produced during the culture is also within the scope of the present invention.
  • the following examples illustrate a specific mutant strain of Clostridium acetobutylicum M5 as a host strain incapable of producing organic solvents, but it will be apparent to one skilled in the art that other microorganisms of the genus Clostridium or of other genera, which have biosynthetic pathways for conversion of acetyl CoA to butyryl CoA and whose pathways for organic solvent biosynthesis are blocked can be used as a host strain, and the same genes can be introduced into the host strain for ethanol and butanol production.
  • Example 1 Preparation of a recombinant vector containing adhEl gene encoding alcohol/aldehyde dehydrogenase, and ctfAB gene encoding CoA transferase
  • the adhEl, ctfA and ctfB genes of Clostridium acetobutylicum ATCC 824 which have the base sequences of SEQ ID NO: 3, SEQ ID NO: 4 and SEQ ID NO: 5, respectively, were cloned together with the promoter and transcription termination sequences thereof.
  • PCR (Table 1) was performed with the primers of SEQ ID NO: 1 and SEQ ID NO: 2, then the obtained adhEl, ctfA and ctfB genes were cut with the restriction enzyme Sail and inserted into Clostridium/E. coli shuttle vector pIMPl (Mermelstein, L.D.
  • the base sequences of the cloned adhEl and ctfAB genes derived from Clostridium acetobutylicum ATCC 824, were analyzed, and the amino acid sequences of alcohol/aldehyde dehydrogenase and CoA transferase were deduced. As the result, the DNA sequences (SEQ ID NO: 3, SEQ ID NO: 4 and SEQ ID NO: 5) and amino acid sequences (SEQ ID NO: 6, SEQ ID NO: 7 and SEQ ID NO: 8) of the adhEl and ctfAB of Clostridium acetobutylicum ATCC 824 were identified.
  • M5(pIMPl ::adhEl . ctfAB) strain was constructed by introducing the recombinant vector pIMPl ::adhEl .ctfAB constructed in Example 1 into Clostridium acetobutylicum M5 strain by electroporation.
  • the recombinant vector of Example 1 was introduced into Escherichia coli TOPlO, which contains the vector p ANl expressing Bacillus subtilis Phage ⁇ 3T I methy transferase (Mermelstein et al, Appl. Environ. Microbiol, 59: 1077, 1993) to induce methylation thereof, such that the vector becomes suitable for transformation into Clostridium.
  • the methylated vector was isolated and purified from E. coli, and then introduced into a mutant strain of Clostridium acetobutylicum M5 (Cornillot et al, J. Bacteriol, 179:5442, 1997) which lacks megaplasmid (carrying 176 genes, including a gene encoding acetoacetic acid decarboxylase, a gene encoding CoA transferase and a gene encoding alcohol/aldehyde dehydrogenase), thus preparing a recombinant microorganism.
  • pIMPl which had been used as a cloning vector, was introduced into Clostridium acetobutylicum M5 strain, thus preparing M5(pIMPl) strain.
  • M5 competent cells were prepared for transformation as follows: First, M5 strain was inoculated into 10m£ of CGM (Table 2) and cultured to an OD of 0.6. The culture broth was inoculated into 60m# of 2X YTG medium (Bacto tryptone 16g, Yeast extract 1Og, NaCl 4g and Glucose 5g per 1 liter) to a concentration of 10% and the cells were cultured for 4-5 hours. The microorganism cells were washed twice with transformation buffer (EPB, 27OmM sucrose 15m£, 686mM NaH 2 PO 4 HO ⁇ , pH 7.4) and then suspended in 2.4ml, of the same buffer.
  • transformation buffer EPB, 27OmM sucrose 15m£, 686mM NaH 2 PO 4 HO ⁇ , pH 7.4
  • the thus prepared 600 ⁇ i of the M5 competent cells were mixed with 25 /z£ of the recombinant plasmid DNA, and the mixture was loaded into a cuvette with a 4mm electrode gap, and then was subjected to electric shock at 2.5 kV and 25uF, followed by suspending immediately in ImI of 2X YTG medium to culture for 3 hours at 37 ° C ; thus, selecting transformants by spreading on a solid 2X YTG medium containing 40 ⁇ g/mi of erythromycin.
  • Example 3 Production of ethanol/butanol using the recombinant microorganism M5(pIMPl : : adhE 1.ctf AB)
  • Example 2 The recombinant microorganism M5(pIMPl ::adhEl.ctfAB) prepared in Example 2 was cultured to examine the performance.
  • CGM medium was sterilized, taken out at a temperature higher than 80 ° C , charged with nitrogen gas, and cooled to room temperature in an anaerobic chamber. Then,
  • the glucose in the medium was measured using a glucose analyzer (model2700 STAT, Yellow Springs Instrument, Yellow Springs, Ohio, USA); and an aliquot of the medium was taken out at various time points in order to measure the concentrations of acetone, ethanol and butanol produced therefrom, using a gas chromatography (Agillent 6890N GC System, Agilent Technologies Inc., CA, USA) equipped with a packed column(Supelco CarbopackTM B AW/6.6% PEG 2OM, 2 m x 2 mm ID, Bellefonte, PA, USA).
  • the present invention has the effect of providing a recombinant microorganism having the ability to produce ethanol and butanol with high yield through the introduction or amplification of specific genes.
  • the recombinant microorganism according to the present invention shows not only almost no production of byproducts such as acetone, but also enhanced ethanol and butanol productivity per unit hour. Accordingly, the inventive microorganism is useful for industrial production of ethanol/butanol.

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EP08865113A 2007-12-20 2008-12-22 Mikroorganismen für erhöhte ethanol- und butanolproduktion sowie verfahren zur herstellung von ethanol und butanol damit Withdrawn EP2222845A4 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020070134701A KR101076042B1 (ko) 2007-12-20 2007-12-20 에탄올 및 부탄올 생성능이 증가된 재조합 미생물 및 이를이용한 에탄올과 부탄올의 제조방법
PCT/KR2008/007577 WO2009082148A2 (en) 2007-12-20 2008-12-22 Enhanced ethanol and butanol producing microorganisms and method for preparing ethanol and butanol using the same

Publications (2)

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EP2222845A2 true EP2222845A2 (de) 2010-09-01
EP2222845A4 EP2222845A4 (de) 2012-03-07

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US (1) US20110027845A1 (de)
EP (1) EP2222845A4 (de)
JP (1) JP2011507504A (de)
KR (1) KR101076042B1 (de)
CN (1) CN101952430B (de)
AU (1) AU2008341277A1 (de)
WO (1) WO2009082148A2 (de)

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DE102008064249A1 (de) * 2008-12-20 2010-07-01 Südzucker Aktiengesellschaft Mannheim/Ochsenfurt Verbesserte Säure- und Lösungsmittelproduktion in Mikroorganismen
KR101346615B1 (ko) * 2009-09-22 2014-01-03 한국과학기술원 부탄올, 에탄올 및 이소프로판올 생성능이 증가된 재조합 변이 미생물 및 이를 이용한 부탄올, 에탄올 및 이소프로판올의 제조방법
US8765446B2 (en) 2009-09-22 2014-07-01 Korea Advanced Institute Of Science And Technology Recombinant mutant microorganisms having increased ability to produce alcohols and method of producing alcohols using the same
KR101284015B1 (ko) * 2009-09-22 2013-07-09 한국과학기술원 부탄올 또는 혼합알코올 생성능 및 아세톤 제거능이 증가된 재조합 변이 미생물 및 이를 이용한 부탄올 또는 혼합 알코올의 제조방법
KR101149882B1 (ko) * 2010-01-15 2012-05-25 한국화학연구원 부탄올 고생산 균주를 이용한 고생산성 부탄올 생산 방법
WO2012045022A2 (en) * 2010-10-01 2012-04-05 The Ohio State University Metabolic engineering of clostridium tyrobutyricum for butanol production
KR101406066B1 (ko) 2012-07-30 2014-06-20 지에스칼텍스 주식회사 부탄올 생성능이 증강된 재조합 미생물 및 이를 이용한 부탄올 생산 방법
KR101473532B1 (ko) 2012-11-20 2014-12-16 지에스칼텍스 주식회사 부탄올 생성능이 증강된 재조합 미생물 및 이를 이용한 부탄올 생산 방법
EP3292174B1 (de) 2015-05-07 2022-09-21 Sun Chemical Corporation Energiehärtbare tintenstrahltinten zur herstellung von schichtverbundstoffen
EP3452606A4 (de) 2016-05-05 2020-01-01 Newpek S.A. De C.V. Enzymatische verfahren zur herstellung von butanol
KR102073308B1 (ko) * 2017-08-29 2020-02-05 광주과학기술원 에탄올 비생산성 아세토젠 균주를 에탄올 생성균주로 전환하는 방법 및 상기 에탄올 생성균주로부터 일산화탄소를 이용한 에탄올의 제조방법
US11142751B2 (en) 2019-03-07 2021-10-12 Auburn University CRISPR-cas system for Clostridium genome engineering and recombinant strains produced thereof
CN110564662B (zh) * 2019-09-30 2022-03-25 南京农业大学 一种整合型高效表达乙醛脱氢酶枯草杆菌的构建方法

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EP2222845A4 (de) 2012-03-07
US20110027845A1 (en) 2011-02-03
KR20090066951A (ko) 2009-06-24
JP2011507504A (ja) 2011-03-10
CN101952430A (zh) 2011-01-19
CN101952430B (zh) 2012-11-28
WO2009082148A2 (en) 2009-07-02
KR101076042B1 (ko) 2011-10-21
AU2008341277A1 (en) 2009-07-02

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